JP2009155207A - Method for crystallizing easily polymerizable compound, and crystallization device - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for crystallizing an easily polymerizable compound, by which the easily polymerizable compound can be stably and continuously crystallized, while preventing the indication failure of a liquid surface detection means due to the adhesion and polymerization of the easily polymerizable compound, and to provide a crystallization device. <P>SOLUTION: Provided is the method for crystallizing the easily polymerizable compound with a crystallization device having a cooling mechanism for exchanging heat through a heat transfer surface, characterized by crystallizing the easily polymerizable compound, while supplying a non-condensable gas to a liquid surface detection means connection pipe for connecting the upper lid of a crystallization tank to a means for detecting a liquid surface, and provided is a device for crystallizing the easily polymerizable compound, characterized by having a cooling mechanism for exchanging heat through a heat transfer surface, a liquid surface detection means for detecting a liquid surface in the crystallization tank, a liquid surface detection means connection pipe for connecting the upper lid of a crystallization tank to a means for detecting a liquid surface, and a non-condensable gas supply pipe for supplying a non-condensable gas to the liquid surface detection means connection pipe. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a crystallization method and a crystallization apparatus for an easily polymerizable compound.

In the case of industrially producing an easily polymerizable compound, a purification process for removing impurities, solvents and the like generated during the production process is indispensable. As such a purification process, extraction, distillation, crystallization, etc. are common, but when the object to be removed is a substance having a high boiling point and a high melting point, or a substance having a high polymerization property, the low temperature region. In many cases, a crystallization method that can be purified to a high purity is used. For example, it is used for purification of crude methacrylic acid obtained by separating methacrylic acid by-produced by ACH method (acetone cyanohydrin method) by extraction or distillation. For example, it is used for the purification of the following crude methacrylic acid. Reaction gas is obtained by subjecting isobutylene, tertiary butyl alcohol, methacrolein or isobutyraldehyde to catalytic gas phase oxidation in which molecular oxygen is contacted in one or two stages. From an aqueous solution obtained by absorbing the reaction gas into water, methacrylic acid is extracted using an organic solvent, and the organic solvent and nonvolatile components are removed by distillation to obtain crude methacrylic acid. Crystallization is used for purification to remove impurities such as aldehydes from the crude methacrylic acid. As a general-purpose crystallization method, there is a crystallization method in which heat exchange is performed through a heat transfer surface.
In the crystallization operation of an easily polymerizable compound using a crystallizer, when continuously crystallizing a crystal from a solution, a liquid level detecting means leading to the inside of the crystallization tank is provided. Detects the liquid level height. By controlling the supply amount of the process fluid supplied into the crystallization tank with respect to the detected liquid level, operation control is performed so as to keep the liquid level constant, thereby improving quality stability and productivity. Yes.
On the other hand, since many easily polymerizable compounds have flammability, if the composition of the gas phase part in the crystallization tank is within the explosion range and an ignition source is present, an explosion reaction can occur. When the easily polymerizable compound falls in the gas phase, static electricity is easily generated due to friction between the liquids, and this static electricity can be an ignition source. For such a problem, a method of controlling the concentration of molecular oxygen within a certain range by substituting the gas phase with an inert gas such as nitrogen so that the composition of the gas phase is outside the explosion range. Is disclosed (for example, Patent Document 1).
JP 2003-342231 A

However, when the crystallization apparatus is operated for a long period of time, in the liquid level detecting means connecting pipe connecting the crystallization tank and the liquid level detecting means, the easily polymerizable compound is polymerized to close the liquid level detecting means connecting pipe, Crystals of easily polymerizable compounds and polymers of easily polymerizable compounds may adhere to the liquid level detecting means. When such clogging or crystal adhesion due to the polymer occurs, it becomes impossible to accurately detect the liquid level in the crystallization tank, which hinders the operation of the crystallization apparatus. For this reason, every time clogging or adhesion of crystals occurs due to the polymer, maintenance work is performed to stop the operation of the crystallizer and remove the polymer or crystals. Such a maintenance work has a problem that it not only lowers productivity but also increases the burden on the operator.
An object of the present invention is to provide a crystallization method and a crystallization apparatus capable of preventing a poor indication of a liquid level detection means due to adhesion or polymerization of an easily polymerizable compound and performing crystallization of the easily polymerizable compound stably and continuously. And

The crystallization method of an easily polymerizable compound according to the present invention is a crystallization method of an easily polymerizable compound using a crystallization apparatus equipped with a cooling mechanism that performs heat exchange through a heat transfer surface. Crystallization is performed while supplying a non-condensable gas to a liquid level detecting means connecting pipe for connecting the upper lid and means for detecting the liquid level.
The non-condensable gas is preferably nitrogen. After the non-condensable gas passes through the pressure control valve and the orifice plate, or after passing through the flow control valve and the flow meter, the liquid level detection means connecting pipe It is preferable to supply to. Moreover, it is preferable that an easily polymerizable compound is methacrylic acid, and it is preferable that the molecular oxygen concentration in the gaseous-phase part inside the said crystallization tank shall be 2-18 volume%.

  The crystallizer for easily polymerizable compounds of the present invention comprises a cooling mechanism for exchanging heat via a heat transfer surface, a liquid level detecting means for detecting the liquid level inside the crystallization tank, and an upper lid of the crystallization tank. And a liquid level detecting means connecting pipe for connecting the liquid level detecting means, and a non-condensable gas supply pipe for supplying non-condensable gas to the liquid level detecting means connecting pipe, and the cooling mechanism Is preferably a cooling jacket.

  According to the present invention, it is possible to prevent an indication failure of the liquid level detection means due to adhesion or polymerization of an easily polymerizable compound and to crystallize the easily polymerizable compound stably and continuously.

An example of an embodiment of the present invention will be described with reference to FIG. However, the present invention is not limited to the following embodiments. In FIG. 1, valves and pumps are omitted as appropriate. For convenience of explanation, the side on which the raw material supply pipe 34 is illustrated is described as “upper”, and the side on which the slurry discharge pipe 36 is illustrated is described as “lower”.
FIG. 1 is a schematic diagram of a crystallizer 10 as an example of an embodiment of the present invention. The crystallization apparatus 10 includes a crystallization tank 12, an upper lid 14, a cooling jacket 16, a liquid level detection means 18, a liquid level detection means connection pipe 20, and a non-condensable gas supply pipe 22. .
An upper lid 14 is placed on the top of the crystallization tank 12, and a cooling jacket 16 is installed outside the crystallization tank 12 from the middle to the bottom. The cooling jacket 16 is connected to a heat source (not shown). And the inner surface of the crystallization tank 12 in which the cooling jacket 16 was installed is a heat-transfer surface. In addition, a stirrer 30 is provided inside the crystallization tank 12, and the stirrer 30 is connected to a power source (not shown).
The liquid level detecting means connecting tube 20 and the temperature detecting means 32 are installed on the upper lid 14 so as to penetrate the upper lid 14, and the liquid level detecting means connecting tube 20 and the lower end portions of the temperature detecting means 32 are both crystallized. It arrange | positions so that it may be located under the liquid level in the analysis tank 12. FIG. A liquid level detection means 18 is connected to the upper end of the liquid level detection means connecting pipe 20. Further, one end of the non-condensable gas supply pipe 22 is connected to the side surface of the liquid level detection means connecting pipe 20, and the other end of the non-condensable gas supply pipe 22 is connected to the flow rate adjusting valve 24. The flow control valve 24 and the flow meter 26 are connected by piping, the flow meter 26 and the pressure reducing valve 28 are connected by piping, and the pressure reducing valve 28 is connected by a piping to a non-condensable gas supply source (not shown). ing.
The raw material supply pipe 34 connected to the upper lid 34 is connected to a raw material supply source (not shown), and the slurry discharge pipe 36 connected to the bottom of the crystallization tank 12 is connected to a next process (not shown).

  The crystallization apparatus main body portion including the crystallization tank 12, the upper lid 14, the cooling jacket 16, and the stirrer 30 is particularly limited as long as it has a cooling mechanism that performs heat exchange through the heat transfer surface. There is nothing. For example, an apparatus described in pages 505 to 520 of “Chemical Engineering Handbook Revised Sixth Edition” (1999) issued by Maruzen Co., Ltd. can be given.

  The cooling jacket 16 is not particularly limited as long as the cooling jacket 16 has a mechanism capable of cooling the compound to be processed through the heat transfer surface by circulating the cooling medium. The cooling mechanism using the cooling jacket 16 is suitable because it can prevent overcooling of the heat transfer surface and has small temperature spots.

  The liquid level detecting means 18 is not particularly limited, and a liquid level gauge such as a displacer type or a spring flow type can be used.

The non-condensable gas supply pipe 22 is not particularly limited as long as it can withstand the pressure when supplying the non-condensable gas. Examples of the material include stainless steel, aluminum, and a rolled steel material subjected to rust prevention processing. Among them, stainless steel pipes are preferable. Some monomers are corrosive, and stainless steel has corrosion resistance.
The flow control valve 24 is not particularly limited, and an existing flow control valve can be used.
Further, the flow meter 26 is not particularly limited, and an existing flow meter can be used.

Next, an example of a crystallization method using the crystallization apparatus 10 will be described.
First, a liquid containing an easily polymerizable compound, which is a compound to be treated (hereinafter sometimes simply referred to as a raw material liquid), is put into the crystallization tank 12 through a raw material supply pipe 34. When the liquid level of the raw material in the crystallization tank 12 reaches a predetermined height, the supply of the raw material liquid is stopped. Next, a non-condensable gas whose flow rate is controlled is supplied to a non-condensable gas supply pipe 22 from a non-condensable gas supply source (not shown) through a pressure reducing valve 28, a flow meter 26, and a flow rate adjusting valve 24. send. The non-condensable gas sent to the non-condensable gas supply pipe 22 flows through the liquid level detection means connecting pipe 20 and is sent into the raw material liquid in the crystallization tank 12. At this time, the non-condensable gas prevents entry of the easily polymerizable compound into the liquid level detecting means connecting pipe 22 and comes into contact with the easily polymerizable compound contained in the raw material liquid. The non-condensable gas that has not been dissolved in the raw material liquid is mixed with the gas in the gas phase in the crystallization tank 12.
While the raw material liquid is stirred by the stirrer 30, a heat medium having an arbitrary temperature is passed through the cooling jacket 16 from a heat source (not shown) to cool the heat transfer surface of the crystallization tank 12. The raw material liquid is cooled by the heat transfer surface of the cooled crystallization tank 12, and finally, it is a temperature at which the crystal of the easily polymerizable compound in the raw material liquid starts to precipitate, or below the crystal precipitation temperature. Cool slowly. And an easily polymerizable compound precipitates from a raw material liquid. When the easily polymerizable compound is precipitated in the crystallization tank 12, a slurry-like process fluid, which is a mixed fluid of the precipitated crystals and the raw material liquid, is obtained.
After the internal temperature of the crystallization tank 12 is stabilized at a predetermined temperature, extraction of the process fluid is started from a discharge port (not shown). At this time, the liquid level detection means 18 detects the liquid level of the liquid phase part, and adjusts the supply amount of the raw material liquid so as to maintain a constant liquid level. In this way, crystals of the easily polymerizable compound are continuously crystallized from the raw material liquid. Thus, the process fluid which has finished the crystallization operation is sent from the crystallization tank 12 to the next step through the slurry discharge pipe 36, and is separated into solid and liquid into crystals and mother liquor. By this solid-liquid separation, purified easily polymerizable crystals can be obtained. For example, when crude methacrylic acid is used as the raw material liquid, purified methacrylic acid is obtained as crystals, and one mother liquor contains the added second component, concentrated impurities, and methacrylic acid that did not precipitate. It is.

  As the easily polymerizable compound, specifically, acrylic acid, methyl acrylate, ethyl acrylate, n-butyl acrylate, hydroxyethyl acrylate, hydroxypropyl acrylate, methacrylic acid, methyl methacrylate, ethyl methacrylate, Examples include n-butyl methacrylate, hydroxyethyl methacrylate, and hydroxypropyl methacrylate. Among them, the effect of the present invention is remarkable in methacrylic acid.

The raw material liquid may contain a polymerization inhibitor in order to prevent polymerization. Examples of the polymerization inhibitor include phenols, hydroquinones, quinones, phenothiazines, amines, N-oxyls, nitric acid compounds and the like. Examples of phenols include 2,4-dimethyl-6-t-butylphenol, examples of hydroquinones include hydroquinone and hydroquinone monomethyl ether, and examples of amines include N, N-di-2-naphthyl-p-phenylenediamine. It is done. These may be used individually by 1 type and may be used in combination of 2 or more type.
The concentration of the polymerization inhibitor is preferably determined according to the type of the easily polymerizable compound. For example, in the case of methacrylic acid, 0.5 to 1000 ppm by mass, 1 to 600 ppm by mass is preferable, and 2 to 500 ppm by mass. Is particularly preferred.

  The type of non-condensable gas is preferably determined in consideration of the type of easily polymerizable compound to be crystallized, the composition of the gas phase in the crystallization tank 12, and the like. For example, examples of the non-condensable gas include nitrogen, oxygen, air, dry air, carbon dioxide, helium, and argon. Among these, nitrogen is preferably used from the viewpoint that it can be easily obtained and the composition of the gas phase part can be easily managed. Non-condensable gas may be used individually by 1 type, and may be used in combination of 2 or more type.

The non-condensable gas may be diluted with another gas (hereinafter referred to as a dilution gas) and used as a mixed gas. In this case, the concentration of the non-condensable gas supplied to the crystallization tank 12 and the flow rates of the non-condensable gas and the mixed gas are not particularly limited, but the molecular oxygen concentration in the gas phase portion of the crystallization tank 12 is It is preferable to determine the concentration and flow rate of the non-condensable gas so that it is preferably 2 to 18% by volume, more preferably 4 to 10% by volume. This is because an unexpected situation can be avoided by keeping the oxygen concentration in the gas phase as far as possible from the explosion limit.
The concentration of the non-condensable gas in the mixed gas is not particularly limited, but is preferably 4 to 10% by volume. If it is less than 4% by volume, it may not be possible to prevent clogging in the liquid level detecting means connecting pipe 20 due to an easily polymerizable compound and adhesion of crystals to the liquid level detecting means 18. On the other hand, if it exceeds 10% by volume, the explosion limit may be temporarily approached due to fluctuations in the supply of non-condensable gas flow.
In addition, the oxygen concentration in the mixed gas is not particularly limited, and can be determined in consideration of the composition of the gas phase portion in the crystallization tank 12. However, if the oxygen concentration in the mixed gas is too low, the oxygen concentration in the gas phase cannot be increased, and if the oxygen concentration is too high, the oxygen concentration in the gas phase cannot be decreased. It is preferable to determine the oxygen concentration in the crystallization tank 12 to be determined.

  The flow rate of the non-condensable gas is not particularly limited, but is preferably determined in consideration of the composition of the gas phase portion of the crystallization tank 12 and the like. If the flow rate of the non-condensable gas is too small, the liquid level detecting means connecting pipe 20 cannot be prevented from being blocked by the easily polymerizable compound in the raw material liquid, and the oxygen concentration in the gas phase cannot be lowered. On the other hand, if the flow rate of the non-condensable gas is too large, the oxygen concentration in the gas phase portion becomes too small to achieve the desired composition. The flow rate of the mixed gas is also preferably determined in consideration of the composition of the gas phase portion of the crystallization tank 12 and the non-condensable gas concentration and oxygen concentration in the mixed gas.

  The temperature at which the raw material liquid is cooled may be equal to or lower than the crystal precipitation temperature at which crystals of the easily polymerizable compound in the raw material liquid begin to precipitate, and should be determined in consideration of the type of easily polymerizable compound and workability, etc. Can do. For example, when the easily polymerizable compound is methacrylic acid (melting point: 15 ° C.), the cooling temperature is preferably set within the range of −10 to 10 ° C. from the viewpoint of operability.

  If necessary, a second component may be added in order to adjust the crystal precipitation temperature of the easily polymerizable compound. For example, when crude methacrylic acid is used as the easily polymerizable compound, the crystal precipitation temperature can be lowered by adding a polar organic substance that does not form a solid solution with methacrylic acid as the second component. Examples of the second component include methanol, ethanol, propanol, butanol and the like. Moreover, the addition amount of a 2nd component has the preferable range of 1-35 mass% with respect to crude methacrylic acid. While the melting point of methacrylic acid is 15 ° C., it is preferable to set the addition amount of the second component so that the crystal precipitation temperature is −10 to 10 ° C.

  The method for separating the crystal and the mother liquor is not particularly limited as long as it is a method capable of separating the solid and the liquid. For example, a known method such as a filtration method or a centrifugal separation method can be used. Specific examples of the apparatus for performing the separation include, for example, Kazuaki Shimizu: “Purification of organic compounds by Kureha continuous crystal purification apparatus”, Chemical Engineering, Vol. 27, No. 3 (1982), p. 49, KCP. Examples thereof include an apparatus. The type of separation operation may be either a batch type or a continuous type.

According to the above embodiment, by crystallizing the easily polymerizable compound while continuously supplying the non-condensable gas to the liquid level detecting means connecting pipe, the composition of the gas phase part is outside the explosion range, The penetration of the easily polymerizable compound into the liquid level detecting means connecting pipe and the polymerization can be suppressed. As a result, it is possible to prevent the polymer from adhering to the liquid level detecting means, and it is possible to prevent the liquid level detecting means from being blocked by the polymerization of the easily polymerizable compound and the crystals from adhering to the liquid level detecting means. In this way, it is possible to prevent defective indication of the liquid level detecting means and to operate the crystallizer stably over a long period of time.
Since maintenance time can be reduced, productivity can be improved and the burden on the operator can be reduced.

In the above embodiment, the non-condensable gas is passed in the order of the flow meter 26 → the flow rate control valve 24, but the order may be reversed.
Further, in the above embodiment, the non-condensable gas is supplied to the liquid level detecting means connecting pipe after passing through the flow rate control valve 24 and the flow meter 26. However, the flow rate control valve is used as a pressure control valve. The flow meter may be replaced with an orifice plate, or none of them may be installed. However, in order to stably control the molecular oxygen concentration in the gas phase in the crystallization tank 12, a non-condensable gas is passed through the flow control valve 24 and the flow meter 26, or the pressure control valve and the orifice plate It is preferable to supply the crystallization tank 12 after passing through a non-condensable gas.

EXAMPLES Hereinafter, although an Example is given and this invention is demonstrated concretely, it is not limited to an Example.
Example 1
Using the crystallization apparatus 10 shown in FIG. 1, crystallization was continuously performed under the following conditions. As the raw material liquid, an easily polymerizable compound-containing liquid of 96.5 to 99.5% by mass of methacrylic acid is used. The raw material liquid is supplied from the raw material supply pipe 34 to the crystallization tank 12, and the raw material liquid temperature is set to 5 to 8 ° C. And the slurry was discharged from the slurry discharge pipe 36. At the same time, nitrogen with an original pressure of 400 kPaG was adjusted by the flow rate adjusting valve 24 so that the flow rate became 5 m ³ (standard state) / h, and then continuously supplied to the liquid level detecting means connecting pipe 20. The non-condensable gas supply pipe 22 was a SUS304 pipe having an inner diameter of 4 mm.

(Comparative Example 1)
The raw material liquid was continuously crystallized in the same manner as in Example 1 except that nitrogen was not supplied to the liquid level detecting means connecting pipe 20.

In Example 1, the liquid level detecting means 18 accurately detected the liquid level of the raw material liquid in the crystallization tank 12 for three months after the operation of the crystallizer 10 was started. Moreover, when the inside of the liquid level detection means 18 and the liquid level detection means connecting pipe 20 was confirmed every 5 days, adhesion of a polymer was not seen.
On the other hand, in Comparative Example 1, it was impossible to accurately detect the liquid level in the crystallization tank when two weeks had passed since the operation was started. When the liquid level detecting means 18 and the liquid level detecting means connecting pipe 20 were removed and the inside was confirmed, a part of the liquid level detecting means connecting pipe 20 was clogged with the polymer.

It is a schematic diagram showing an example of the crystallization apparatus of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 10 Crystallizer 12 Crystallization tank 14 Top cover 16 Cooling jacket 18 Liquid level detection means 20 Liquid level detection means connection pipe 22 Non-condensable gas supply pipe 24 Flow control valve 26 Flow meter

Claims (8)

  A method for crystallizing an easily polymerizable compound using a crystallizer equipped with a cooling mechanism for exchanging heat through a heat transfer surface, which connects an upper lid of the crystallizer and a means for detecting the liquid level A crystallization method of an easily polymerizable compound, characterized in that crystallization is performed while supplying a non-condensable gas to the connecting pipe of the liquid level detection means.   The method for crystallizing an easily polymerizable compound according to claim 1, wherein the non-condensable gas is nitrogen.   The method for crystallizing a readily polymerizable compound according to claim 1 or 2, wherein the non-condensable gas is supplied to a liquid level detecting means connecting pipe after passing through a pressure control valve and an orifice plate.   The method for crystallizing an easily polymerizable compound according to claim 1 or 2, wherein the non-condensable gas is supplied to the liquid level detecting means connecting pipe after passing through a flow rate control valve and a flow meter.   The method for crystallizing an easily polymerizable compound according to any one of claims 1 to 4, wherein the easily polymerizable compound is methacrylic acid.   Crystals of the easily polymerizable compound according to any one of claims 1 to 5, wherein a molecular oxygen concentration in a gas phase portion inside the crystallization tank is 2 to 18% by volume. Analysis method.   Cooling mechanism for exchanging heat through the heat transfer surface, liquid level detection means for detecting the liquid level inside the crystallization tank, and liquid level detection for connecting the upper lid of the crystallization tank and the liquid level detection means A crystallizing apparatus for an easily polymerizable compound, comprising: a means connecting pipe; and a non-condensable gas supply pipe for supplying a non-condensable gas to the liquid level detecting means connecting pipe.   8. The crystallizer for easily polymerizable compounds according to claim 7, wherein the cooling mechanism is a cooling jacket.

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